WO2008078055A2

WO2008078055A2 - Copolymers based on methacrylate units, preparation method thereof and use of same

Info

Publication number: WO2008078055A2
Application number: PCT/FR2007/052589
Authority: WO
Inventors: Laurence Couvreur; Stéphanie Magnet
Original assignee: Arkema France
Priority date: 2006-12-22
Filing date: 2007-12-20
Publication date: 2008-07-03
Also published as: FR2910475B1; FR2910475A1; US8389643B2; WO2008078055A9; EP2113000A2; WO2008078055A3; JP2010513648A; US20100069577A1; TW200838882A

Abstract

The invention relates to a method for preparing a copolymer having a backbone based on methacrylate units, comprising a step involving the polymerisation of one or more precursor methacrylate monomers of said units in the presence of: a polymerisation initiator, at least one RAFT-type transfer agent which can generate a primary radical, and at least one comonomer selected from among styrene monomers and acrylate monomers. The invention also relates to the resulting copolymers, in particular block copolymers, and to the use thereof as additives for plastic materials.

Description

COPOLYMERS BASED ON METHACRYLATE UNITS, PROCESS FOR THEIR PREPARATION AND USES THEREOF

DESCRIPTION

TECHNICAL AREA

The present invention relates to a controlled radical polymerization process of one or more methacrylate monomers in the presence of at least one comonomer and at least one particular transfer agent.

The general field of the invention is that of controlled radical polymerization.

Controlled radical polymerization, through the use of transfer agents, makes it possible to reduce the deactivation reactions of the growing radical species, in particular the termination stage, reactions which, in conventional radical polymerization, interrupt the reaction. polymer chain growth irreversibly and without control.

In order to reduce the probability of termination reactions, it has been proposed to transiently and reversibly block the growing radical species, forming so-called stable "intermediate radical" species. This thus makes it possible to restart the polymerization and to obtain an alternation between periods of growth of active radical species and periods of growth cessation during which these radical species are dormant. This alternation leads to a gradual increase in the average molecular weight as a function of the progress of the polymerization reaction, which therefore takes place in a controlled manner. This control often results in a narrower polymer molecular weight distribution (and therefore a lower polymolecularity index) than in conventional radical polymerization. This also makes it possible to synthesize block copolymers by reactivating the polymerization with a new monomer from a dormant polymer species.

One particular type of controlled radical polymerization is the so-called "RAFT" polymerization (which corresponds to the English terminology "Reversible Addition Fragmentation Transfer"), which uses sulfur-containing compounds as transfer agents to give polymers having a controlled architecture, particularly at level of the polymolecularity index.

Such transfer agents are for example described in US 6,512,081, WO 98/01478, WO 99/31144, EP 825.247.

The so-called "RAFT" polymerization makes it possible to obtain polymers with a polymolecularity index or polydispersity that is significantly lower than that obtained for polymers obtained by a conventional radical polymerization process (without chain transfer agent "RAFT").

This type of polymerization has in particular already been implemented to develop homopolymers comprising methacrylate units such as polymethyl methacrylate (PMMA) with a dithiobenzoate-type transfer agent generating a secondary or tertiary radical, the agents generating tertiary radicals being Macromolecules, 2005, 38-3129-3140, Macromolecules, 2003, 36-2256-2272) or Examples 19 and 20 of WO 98/01478 are styrenic polymers, such as PS, prepared in the presence of primary transfer, dibenzyl trithiocarbonate (DBTTC) in Example 23 of WO 98/01478; or in the presence of a secondary RAFT agent, 1-phenylethyl phenyldithioacetate (cf Journal of Polymer Science, part A, vol 42, 6248-6258 (2004) which also describes the synthesis of PMMA and the styrene-MAM random copolymer, the polydispersity index of the PS is low but that of the PMMA is very high and it increases for the copolymer with the level of MAM present in the copolymer. as well as styrene-MAM block copolymers described for example in Polymer 46 (2005) 9762-9768 where they are synthesized in the presence of a secondary transfer agent RAFT (1-phenylethyl phenyldithioacetate) or tertiary transfer agent (cumyl dithioacetate), statistical MAM-styrene, MMA-butyl acrylate copolymers in the presence of a tertiary RAFT transfer agent (cumyl dithioacetate).

However, until now, the methacrylate polymers obtained from this type of transfer agent have a low polymolecularity index but to obtain a conversion rate of the acceptable polymerization reaction, typically greater than or equal to 50 % and preferably greater than 60%, it is then necessary to extend the duration of the polymerization to several tens of hours.

Thus, the inventors have set themselves the goal of developing a process for preparing a copolymer based on methacrylate units making it possible to obtain a copolymer generally having a polymolecularity index of less than or equal to 2, or any at least less than that obtained with the radical polymerization processes of the prior art.

They have thus surprisingly found that by polymerizing the methacrylate monomer or monomers in the presence of at least one particular transfer agent and at least one particular comonomer, it was possible to reduce the polymolecularity index of the copolymers obtained, compared to the polymolecularity index of the polymers obtained without the presence of said comonomer, with a degree of conversion of the polymerization reaction of more than 50% generally obtained after less than 10 hours.

STATEMENT OF THE INVENTION

Thus, the invention relates, according to a first object, to a process for preparing a copolymer comprising a skeleton based on methacrylate units, comprising a step of polymerizing one or more precursor methacrylate monomers of said units in the presence of:

at least one polymerization initiator;

at least one transfer agent of the "RAFT" type capable of generating a primary radical (referred to simply as the following primary agent) of formula

where R is CH ₂ R 1 with R 1 selected from the group consisting of optionally substituted alkyl; a saturated, unsaturated or aromatic carbocyclic or heterocyclic ring, optionally substituted; an optionally substituted alkylthio group, an optionally substituted alkoxy group; an optionally substituted dialylamino group; an organometallic substance; and a polymer chain prepared by any polymerization mechanism; a free radical liberating radical R ^' which initiates the free radical polymerization wherein Z is selected from the group consisting of hydrogen, chlorine, an optionally substituted alkyl group, an optionally substituted aryl group, of an optionally substituted heterocycle group, an optionally substituted alkylthio group -SR2, an optionally substituted alkoxycarbonyl group, a optionally substituted aryloxycarbonyl (-COOR2), a carboxy group (-COOH), an optionally substituted acyloxy group (-OOCR2), a carbamoyl group (-CON R2) optionally substituted with a cyano group (-CN ), a dialkyl- or diarylphosphonato [-P (= O) OR2 ₂ ] group, a dialkyl- or diarylphosphinato [-P (= O) R2 ₂ ] group and a polymer chain prepared by a any polymerization, a -0R2 group, an -NR2R3 group wherein R2 and R3, identical or different, are selected from the group consisting of alkyl, Ci to C ₈ optionally substituted; an alkenyl C ₂ to C _8, an aryl group, a heterocyclyl group, an aralkyl group, an alkaryl group, wherein the substituents are independently selected from the group consisting epoxy, hydroxy, alkoxy, acyl, acyloxy, carboxy (and its salts), sulfonic acid (and its salts), alkoxy or aryloxycarbonyl, isocyanato, cyano, silyl, halo and dialkylamino;

; and at least one comonomer selected from styrene monomers, acrylic monomers such as acrylic acid and its salts, acrylonitrile, acrylamide or substituted acrylamides, 4-acryloylmorpholine, N-methylolacrylamide, chloride acrylamidopropyltrimethylammonium (APTAC), acrylamidomethylpropanesulfonic acid (AMPS) or its salts, methacrylamide or substituted methacrylamides, N-methylolmethacrylamide, methacrylamidopropyltrimethylammonium chloride (MAPTAC), itaconic acid, maleic acid or its salts, maleic anhydride, alkyl or alkoxy- or aryloxy-polyalkylene glycol maleates or hemimaleate, vinylpyridine, vinylpyrrolidinone, (alkoxy) poly (alkylene glycol) vinyl ether or divinyl ether, such as methoxy poly (ethylene glycol) vinyl ether, poly (ethylene glycol) divinyl ether, olefinic monomers, among which mention may be made of ethylene, propylene, butene, hexene and 1-octene as well as fluorinated olefinic monomers, and vinylidene monomers, among which mention may be made of vinylidene fluoride, preferably vinylidene chloride, alone or as a mixture.

By way of examples of methacrylate units, mention may be made of methacrylic monomers such as methacrylic acid or its salts, alkyl, cycloalkyl, alkenyl or aryl methacrylates, such as methyl methacrylate and lauryl methacrylate. , cyclohexyl, allyl or phenyl, hydroxyalkyl methacrylates such as 2-hydroxyethyl methacrylate or 2-hydroxypropyl methacrylate, ether alkyl methacrylates such as 2-ethoxyethyl methacrylate, methacrylates of alkoxy- or aryloxy-polyalkyleneglycols such as methoxypolyethylene glycol methacrylates, ethoxypolyethylene glycol methacrylates, methoxypolypropylene glycol methacrylates, methoxy-polyethyleneglycol-polypropylene glycol methacrylates or mixtures thereof, aminoalkyl methacrylates such as 2- (dimethylamino) methacrylate ) (Ammethyl), amine salt methacrylates such as chloride or sulfate of

(methacryloyloxy) ethyl] trimethylammonium or chloride or sulphate

(methacryloyloxy) ethyl] dimethylbenzylammonium, fluorinated methacrylates such as 2,2,2-trifluoroethyl methacrylate, silylated methacrylates such as 3-methacryloylpropyltrimethylsilane, phosphorus methacrylates such as alkylene glycol phosphate methacrylates, methacrylate of hydroxyethylimidazolidone, methacrylate hydroxyethylimidazolidinone, 2- (2-oxo-1-imidazolidinyl) ethyl methacrylate.

As examples of styrenic monomers, mention may be made of styrene or substituted styrenes, especially α-methylstyrene, sodium styrene sulphonate or bromostyrene.

As examples of acrylic monomers, there may be mentioned acrylic acid or its salts, alkyl, cycloalkyl or aryl acrylates such as methyl acrylate, ethyl acrylate, butyl acrylate, ethylhexyl acrylate and the like. or phenyl, hydroxyalkyl acrylates such as 2-hydroxyethyl acrylate, alkyl ether acrylates such as 2-methoxyethyl acrylate, alkoxy- or aryloxy-polyalkylene glycol acrylates such as methoxypolyethylene glycol acrylates ethoxypolyethylene glycol acrylates, methoxypolypropylene glycol acrylates, methoxypolyethylene glycol-polypropylene glycol acrylates or mixtures thereof, aminoalkyl acrylates such as acrylate

(dimethylamino) ethyl (ADAME), amine salt acrylates such as chloride or sulfate of [2-

(acryloyloxy) ethyl] trimethylammonium or [2- (acryloyloxy) ethyl] dimethylbenzylammonium chloride or sulfate, fluorinated acrylates, silylated acrylates, phosphorus acrylates such as alkyleneglycol phosphate acrylates.

Among the chain transfer agents, there may be mentioned dithioesters, dithiocarbonates or xanthates, dithiocarbamates and trithiocarbonates that can be represented by one of the formulas below: R ¹ . .S- RR ¹ - O- -S- R -S- RR ¹ - S. -S- R ssss

Dith ioester Dithiocarboπ ate Dithiocarbamate Tπthiocarboπ ate

(= xaπth ate)

Dithioesters which can be advantageously used in the context of the invention are those corresponding to the following formula (I):

(I)

in which Z represents a group selected from -

C ₆ H ₅ , -CH ₃ , a pyrrole group, -OC ₆ F ₅ , a pyrrolidinone group, -OC ₆ H ₅ , -OC ₂ H ₅ , -N (C ₂ H ₅ ) ₂ , and advantageously the group - S CH ₂ -C ₆ H ₅ (dibenzyl trithiocarbonate of formula

(II) following:

(Ii:

Generally, the transfer agent is added in an amount ranging from 0.1% to 20% by weight relative to the mass of monomer (s), preferably from 0.1% to 15% and even more preferentially from 0, 25% to 10%.

In addition to the transfer agent, the polymerization medium also comprises at least one initiator of polymerization. By polymerization initiator is conventionally meant a chemical species capable of producing free radicals which will add to the monomers to produce propagating radicals, from which the polymerization can propagate. The initiators used may choose organic or inorganic peroxides, azo compounds, redox couples and / or alkoxyamines.

By way of examples of azo compounds, mention may be made of 2,2'-azobis (isobutyronitrile), 2,2'-azobis (2-cyano-2-butane) and dimethyl-2,2'-azobis ( methylisobutyrate), 4,4'-azobis (4-cyanopentanoic acid), 4,4'-azobis (4-cyanopentan-1-ol), 1,1'-azobis (cyclohexanecarbonitrile), 2,2 ' azobis [2-methyl-N- (1,1) -bis (hydroxymethyl) -2-hydroxyethyl] propianamide, 2,2'-azobis [2-methyl-N-hydroxyethyl] propianamide, hydrochloride of 2, 2'-azobis (N, N'-dimethyleneisobutyramidine), 2,2'-azobis (2-amidinopropane) hydrochloride, 2,2'-azobis (N, N'-dimethyleneisobutyramine), 2,2 ' azobis (2-methyl-N- [1,1-bis (hydroxymethyl) -2-hydroxyethyl] propionamide), 2,2'-azobis (2-methyl-N- [1,1-bis (hydroxymethyl) ethyl) propionamide), 2,2'-azobis (2-methyl-N- (2- (hydroxyethyl) -propionamide), 2,2'-azobis (isobutyramide) hydride, 2,2'-azobis ( 2, 2, 4-trimethylpentane) 2, 2'-azobis (2-methylpropane).

Examples of peroxide compounds that may be mentioned include t-butyl peroxyacetate, t-butyl peroxybenzoate, t-butyl peroxyoctoate, t-butyl peroxyneodecanoate, t-butyl peroxyisobutyrate, peroxypivalate and the like. t-amyl, t-butyl peroxypivalate, di-isopropyl peroxydicarbonate, dicyclohexyl peroxydicarbonate, dicumyl peroxide, dibenzoyl peroxide, dilauroyl peroxide, potassium peroxydisulfate, ammonium peroxydisulfate. As examples of nitrite compounds, mention may be made of di-t-butyl hyponitrite, dicumyl hyponitrite.

Generally, the polymerization initiator is added in an amount ranging from 1% to 50% by weight relative to the mass of transfer agent, preferably from 2% to 35% and even more preferentially from 5% to 20%.

The presence of the comonomers in addition to the transfer agents as defined above advantageously makes it possible to reduce the polymolecularity index of the copolymers obtained.

These comonomers are advantageously introduced into the polymerization medium in a content not exceeding 50% by weight relative to the methacrylic monomer, for example ranging from 10% to 40% and preferably from 1% to 25%.

The process for preparing the copolymer based on methacrylate units according to the invention can be carried out by solvent, by mass, in dispersed media (such as emulsion, suspension). The emulsion may be a miniemulsion or a microemulsion.

When the polymerization proceeds in emulsion, at least one emulsifying agent, that is to say a surfactant for stabilizing the emulsion, may be added to the polymerization medium. Any emulsifying agent usual to this kind of emulsion can be used.

The emulsifying agent may be anionic, cationic or nonionic. The emulsifying agent may be an amphoteric or quaternary or fluorinated surfactant. It may be chosen from alkyl or aryl sulphates, alkyl or aryl sulphonates, fatty acid salts, polyvinyl alcohols and polyethoxylated fatty alcohols. As for example, the emulsifying agent can be chosen from the following list:

sodium lauryl sulphate,

sodium dodecylbenzenesulphonate,

- sodium stearate,

- nonylphenolpolyethoxylated,

sodium dihexylsulfosuccinate,

sodium dioctylsulfosuccinate,

- lauryl dimethyl ammonium bromide,

- lauryl amido betaine,

perfluoro octyl potassium acetate.

The emulsifying agent may also be an amphiphilic block or random or graft copolymer, such as copolymers of sodium styrene sulphonate and in particular sodium polystyrene-b-poly (sodium styrene sulphonate) or any amphiphilic copolymer prepared by any other polymerization.

The emulsifying agent may be introduced into the polymerization medium in a proportion of 0.1% to 10% by weight relative to the mass of monomer (s).

Generally, the process of the invention is carried out at a temperature ranging from 20 ° C to 200 ° C, preferably from 40 ° C to 150 ° C and more preferably from 50 ° C to 120 ° C.

The subject of the present invention is also the copolymers based on methacrylate units that can be obtained according to the preparation method defined above and more particularly the copolymers, in which the monomer is methyl methacrylate, the comonomer is the acrylate of n-butyl and / or styrene, the transfer agent being preferably a trithiocarbonate, such as dibenzyl trithiocarbonate. The process of the invention is a controlled and living radical process, insofar as it has been found that:

the number-average molecular weight (Mn) as a function of the conversion of the monomers to polymers evolves in a linear manner and the natural logarithm of the ratio (M _o / M) (M ₀ representing the initial concentration of monomer (s) and M representing the concentration of monomers at a given instant of the polymerization) evolves linearly with time; it is possible to reinitiate at least a portion of the polymer chains obtained by this process by the addition of a monomer to make a block grafted to the living polymer obtained.

It is therefore quite natural that the process of the invention mentioned above applies to the preparation of block copolymers.

Thus, the invention relates, according to a third object, to a process for the preparation of a block copolymer comprising at least one block comprising methacrylate units resulting from the polymerization of one or more methacrylate monomers, called block A, in which or said blocks A are prepared by carrying out the process for preparing the copolymer based on methacrylate units as defined above, the copolymer thus being integrated into the block copolymer in the form of a block.

Because of the living nature of this block, one can thus access a very large number of architectures of block copolymers, according to the order of introduction of the constituent monomers of each of the blocks and the nature of the initiator and control agent used.

Thus, according to the invention, copolymers comprising at least one block A and at least one block B, interconnected by a covalent bond, by a process comprising successively: a) a step of implementing the method as defined above; b) a step of adding the constituent monomers of block B.

Between steps a) and b) there may be provided a step of removing unreacted residual monomers in step a).

The constituent monomers of the block B may be chosen from methacrylate monomers different from those used in block A, optionally comprising acid, anhydride, hydroxy, amine, poly (ethylene glycol), poly (ethylene oxide), acrylate monomers functionalities. , optionally comprising functionalities as defined above, styrenic monomers and mixtures thereof.

By virtue of the implementation of step a), it is possible to obtain block copolymers having a polymolecularity index close to 2, this characteristic thus making it possible to obtain products with improved rheology going into applications such as lubricants, rheology modifiers for varnishes, paints, coatings, dispersants.

The control of the polymerization of the methacrylate monomers opens up the possibility of preparing high molecular weight copolymers, which may prove to be beneficial as a processing aid for the processing of thermoplastics, polyvinyl chloride, for example.

The block copolymers that can be prepared according to the invention can be ternary copolymers (that is to say comprising three blocks), these ternary copolymers, which can in particular be used as additives polymeric. These copolymers can for example act as compatibilizers of matrices of different nature, and this thanks to the presence of the end blocks of different chemical nature, while possibly playing the role of shock additive if the central block is chosen in the family of elastomers.

The invention will now be described with respect to the following examples given for illustrative and not limiting.

BRIEF DESCRIPTION OF THE DRAWINGS

Figure 1 is a graph illustrating the conversion rate as a function of time for different mixtures (n-butyl acrylate / methyl methacrylate).

Figure 2 is a graph illustrating the conversion rate as a function of time for different mixtures (styrene / methyl methacrylate).

DETAILED PRESENTATION OF PARTICULAR EMBODIMENTS

COMPARATIVE EXAMPLE 1

This example illustrates the polymerization of methyl methacrylate in solution in the presence of dibenzyl trithiocarbonate (DBTTC).

In a polymerization reactor equipped with a variable speed stirring motor, inputs for the introduction of reagents, taps for the introduction of inert gases for the removal of oxygen, such as nitrogen, and measurement probes (for example, temperature sensors), a reflux condenser system, a jacket for heating / cooling the contents of the reactor by circulating a coolant therein, 150 g of methyl methacrylate (ie 1.5 moles) are introduced, 150 g of methoxypropyl acetate (ie 1.14 mol), 0.038 g of azobisisobutyronitrile (ie 0.231 mol) and 0.658 g of dibenzyl trithiocarbonate (ie 2.27 mmol).

After several degassings with nitrogen, the reaction medium is brought to 80 ° C. and this temperature is maintained by thermal regulation for several hours. Samples are taken throughout the reaction in order to:

- determine the kinetics of gravimetric polymerization (measurement of dry extract);

- follow the evolution of the number average molecular weight (Mn) as a function of the conversion of monomer to polymer.

After 6 h, a conversion of 56% is reached and the reaction medium is cooled to ambient temperature and then withdrawn from the reactor and the residual monomers and solvents are removed by evaporation under vacuum.

The molecular weights of poly (methyl methacrylate) PMMA equivalent determined by steric exclusion chromatography are 147,000 g / mol for the number average molecular weight (Mn) and 420,000 g / mol for the weight average molecular weight (Mw). ). The polymolecularity index is 2.87.

COMPARATIVE EXAMPLE 2

This example illustrates the polymerization of n-butyl acrylate in solution in the presence of dibenzyl trithiocarbonate (DBTTC).

The procedure is identical to that mentioned in Example 1. 150 g of n-butyl acrylate (ie 1.17 moles), 150 g of methoxypropyl acetate (ie 1.13 moles), 0.038 g are added. azo-bis-isobutyronitrile (ie 0.231 moles) and 0.659 g of dibenzyl trithiocarbonate (ie 2.27 mmol). After 4 h, a conversion of 93% is reached and the reaction medium is cooled to ambient temperature and then withdrawn from the reactor and the residual monomers and solvents are removed by evaporation under vacuum.

The molecular weights of poly (n-butyl acrylate) in polystyrene equivalents determined by steric exclusion chromatography are 36,000 g / mol for the number-average molar mass (Mn) and 53,000 g / mol for the average molar mass by weight. (Mw). The polymolecularity index is 1.55.

COMPARATIVE EXAMPLE 3

This example illustrates the bulk polymerization of styrene in the presence of dibenzyl trithiocarbonate (DBTTC).

The procedure is identical to that mentioned in Example 1. 300 g of styrene (ie 2.88 mol), 0.0747 g of azobisisobutyronitrile (ie 0.455 mol) and 1.32 g of trithiocarbonate are introduced. dibenzyl (ie 4.54 mmol).

After 6 h, a conversion of 21% is reached and the reaction medium is cooled to ambient temperature and then withdrawn from the reactor and the residual monomers and solvents are removed by evaporation under vacuum.

The molecular weights of the polystyrene equivalent of polystyrene determined by steric exclusion chromatography are 11300 g / mol for the number-average molecular weight (Mn) and 16000 g / mol for the weight-average molar mass (Mw). . The polymolecularity index is 1.41.

EXAMPLE 4 ACCORDING TO THE INVENTION

This example illustrates, according to the invention, the polymerization of methyl methacrylate in the presence of dibenzyl trithiocarbonate (DBTTC) and n-butyl acrylate. The procedure is identical to that mentioned in Example 1. Xg of methyl methacrylate and Yg of n-butyl acrylate (such as X + Y = 150 g), 150 g of methoxypropyl acetate (ie 1 , 14 moles), 0.038 g of azobisisobutyronitrile (ie 0.233 mmol) and 0.661 g of dibenzyl trithiocarbonate (ie 2.28 mmol).

At the end of the reaction, the reaction medium is cooled to room temperature and then withdrawn from the reactor and the residual monomers and solvents are removed by evaporation under vacuum. Figure 1 illustrates the evolution of the conversion over time according to the type of mixture.

The molecular weights of the polymers thus obtained, as a function of the ratio (n-butyl acrylate / methyl methacrylate), as polymethyl methacrylate equivalent determined by steric exclusion chromatography are listed in the table below.

With a substantially equal polymerization time, a decrease in the polymolecularity index for the examples according to the invention is thus observed when the amount of n-butyl acrylate increases. EXAMPLE 5 ACCORDING TO THE INVENTION

This example illustrates, according to the invention, the polymerization of methyl methacrylate in the presence of dibenzyl trithiocarbonate (DBTTC) and styrene.

The procedure is identical to that mentioned in Example 1. Xg of methyl methacrylate and Yg of styrene (such as X + Y = 300), 0.075 g of azobisisobutyronitrile (ie 0.456 mmol) are introduced and 1.321 g of dibenzyl trithiocarbonate (ie 4.55 mmol).

At the end of the reaction, the reaction medium is cooled to room temperature and then withdrawn from the reactor and the residual monomers and solvents are removed by evaporation under vacuum. Figure 2 illustrates the evolution of the conversion over time according to the type of mixture.

The molecular weights of the polymers thus obtained, as a function of the ratio (styrene / methyl methacrylate), as polymethyl methacrylate equivalent determined by steric exclusion chromatography are listed in the table below.

With a substantially equal polymerization time, a decrease in the polymolecularity index is observed for the examples according to the invention, when the amount of styrene increases.

Claims

22

ethoxypolyethylene glycol methacrylates, methoxypolypropylene glycol methacrylates, methoxy-polyethylene glycol-polypropylene glycol methacrylates or mixtures thereof, aminoalkyl methacrylates such as 2- (dimethylamino) ethyl methacrylate (MADAME), amino salt methacrylates such as that [2- (methacryloyloxy) ethyl] trimethylammonium chloride or sulfate or [2-

(methacryloyloxy) ethyl] dimethylbenzylammonium, fluorinated methacrylates such as 2,2,2-trifluoroethyl methacrylate, silylated methacrylates such as 3-methacryloylpropyltrimethylsilane, phosphorus methacrylates such as alkylene glycol phosphate methacrylates, methacrylate of hydroxyethylimidazolidone, hydroxyethylimidazolidinone methacrylate, 2- (2-oxo-1-imidazolidinyl) ethyl methacrylate.

5. Preparation process according to any one of the preceding claims, wherein the styrenic monomers are selected from styrene and / or substituted styrenes including α-methylstyrene, sodium styrene sulfonate, bromostyrene.

6. Preparation process according to any one of the preceding claims, wherein the acrylic monomers are chosen from acrylic acid or its salts, alkyl acrylates, cycloalkyl or aryl such as methyl acrylate, ethyl acrylate, butyl acrylate, ethylhexyl acrylate, phenyl acrylate, hydroxyalkyl acrylates such as 2-hydroxyethyl acrylate, alkyl ether acrylates such as 2-methoxyethyl acrylate, alkoxy acrylates, and the like. or aryloxy-polyalkylene glycol such as methoxypolyethylene glycol acrylates, ethoxypolyethylene glycol acrylates, methoxypolypropylene glycol acrylates, methoxypolypropylene glycol acrylates, 23

polyethylene glycol-polypropylene glycol or mixtures thereof, aminoalkyl acrylates such as acrylate

7. Preparation process according to any one of the preceding claims, wherein the transfer agent is added in an amount ranging from 0.1% to 20% by weight relative to the mass of monomer (s), preferably from 0.1% to 15% and even more preferably 0.25% to 10%.

8. Process for the preparation of a block copolymer comprising at least one block comprising methacrylate units resulting from the polymerization of one or more methacrylate monomers, called block A, in which the said block or blocks A are prepared by the implementation of the method as defined in any one of claims 1 to 7.

9. Copolymers obtainable according to any one of claims 1 to 8.

The copolymer of claim 9, wherein the methacrylate monomer is methyl methacrylate, the comonomer is n-butyl acrylate, and the transfer agent is preferably dibenzyl trithiocarbonate.

The copolymer of claim 9, wherein the monomer is methyl methacrylate, the comonomer is styrene and the transfer agent is preferably dibenzyl trithiocarbonate.

12. Use of the copolymers of claims 9 to 11 as processing aids for the transformation of 24

thermoplastics, such as polyvinyl chloride, for example.

13. Use of the block copolymers of claims 9 to 11 as polymeric additives, such as compatibilizers matrixes of different nature and / or impact additives.

25

DESCRIPTIVE ABSTRACT

The invention relates to a process for preparing a copolymer comprising a skeleton based on methacrylate units comprising a step of polymerizing one or more precursor methacrylate monomers of said units in the presence of:

a polymerization initiator;

at least one transfer agent of the "RAFT" type that is capable of generating a primary radical; and

at least one comonomer chosen especially from styrene monomers and acrylate monomers.

The invention also relates to the copolymers that can be obtained according to this process, in particular block copolymers and their uses as additives for plastics.

DESCRIPTION

TECHNICAL AREA

This type of polymerization has in particular already been implemented to develop homopolymers comprising methacrylate units such as polymethyl methacrylate (PMMA) with a dithiobenzoate-type transfer agent generating a secondary or tertiary radical, the agents generating tertiary radicals being Macromolecules, 2005, 38-3129-3140, Macromolecules, 2003, 36-2256-2272) or Examples 19 and 20 of WO 98/01478 are styrenic polymers, such as PS, prepared in the presence of primary transfer, dibenzyl trithiocarbonate (DBTTC) in Example 23 of WO 98/01478; or in the presence of a secondary RAFT agent, 1-phenylethyl phenyldithioacetate (cf Journal of Polymer Science, part A, vol 42, 6248-6258 (2004) which also describes